WO2013019111A1 - Utilisation d'un condensat de torréfaction - Google Patents

Utilisation d'un condensat de torréfaction Download PDF

Info

Publication number
WO2013019111A1
WO2013019111A1 PCT/NL2012/050541 NL2012050541W WO2013019111A1 WO 2013019111 A1 WO2013019111 A1 WO 2013019111A1 NL 2012050541 W NL2012050541 W NL 2012050541W WO 2013019111 A1 WO2013019111 A1 WO 2013019111A1
Authority
WO
WIPO (PCT)
Prior art keywords
biomass
btc
torrefaction
solid
torrefied
Prior art date
Application number
PCT/NL2012/050541
Other languages
English (en)
Inventor
Robin Willem Rudolf Zwart
Jan Remmert Pels
Original Assignee
Stichting Energieonderzoek Centrum Nederland
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from NL2007206A external-priority patent/NL2007206C2/en
Application filed by Stichting Energieonderzoek Centrum Nederland filed Critical Stichting Energieonderzoek Centrum Nederland
Publication of WO2013019111A1 publication Critical patent/WO2013019111A1/fr

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
    • C10L5/10—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders
    • C10L5/14—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/26—After-treatment of the shaped fuels, e.g. briquettes
    • C10L5/32—Coating
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/34—Other details of the shaped fuels, e.g. briquettes
    • C10L5/36—Shape
    • C10L5/361—Briquettes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/34—Other details of the shaped fuels, e.g. briquettes
    • C10L5/36—Shape
    • C10L5/363—Pellets or granulates
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/08—Treating solid fuels to improve their combustion by heat treatments, e.g. calcining
    • C10L9/083—Torrefaction
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/10—Treating solid fuels to improve their combustion by using additives
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • the invention is in the field of torrefaction of biomass.
  • the invention is also in the field of producing solid fuels as well as chemicals and materials.
  • Torrefaction is a technique for producing valuable materials such as fuel, from wood or biomass waste such as plant residues from agriculture or sylviculture. Torrefaction is a thermal treatment at moderate temperatures in the substantial absence of oxygen. Torrefaction is distinguished from pyrolysis by the temperatures used: while pyrolysis employs temperatures of 300-700°C, in particular 400-500°C, the temperatures used in torrefaction are between 200 and 350°C.
  • US 2010/0083530 discloses a torrefaction process wherein wet cellulose material is cascaded down a torrefaction reactor to produce steam and volatiles, in addition to a dried solid.
  • the volatiles can be used for their calorific value.
  • torrefied fuel is densified. It is done for several reasons. Primarily, it improves logistics (transport and storage), but it also leads to efficient feeding in combustion and gasification installations. Densification is done by mechanical compression, e.g. pelleting, briquetting and tabletting. In densification, binder may be added to improve the cohesion of the material and the resistance against wear or breakage. The binder also acts as a lubricant in the compression, lowering energy consumption of the machine and diminishing porosity, thus increasing density.
  • the invention pertains to the use of a biomass torrefaction condensate (BTC) as a binding agent or coating agent for solid material, as well as to its use as either bio-based chemical or material or bio-based additive to chemical or material.
  • BTC biomass torrefaction condensate
  • the invention furthermore pertains to a process for producing a wear- and water-resistant solid fuel, comprising combining a solid carbonaceous material with a BTC obtained by condensation of organic material volatilised during torrefaction of biomass.
  • the solid material is biomass-derived, such as torrefied biomass.
  • the invention in particular concerns a process for upgrading biomass comprising:
  • step (b) combining the condensate of step (b) with a torrefied solid fraction, of step (a) or of another process;
  • step (a) densifying the torrefied solid fraction of step (a) (prior to step (a)) or step (c) (after step (c)).
  • step (c) preferably comprises coating the torrefied solid fraction of step (d).
  • a further step my comprise tuning and/or upgrading the condensate of step (b).
  • the invention pertains to the (partially) biomass-derived products including solid fuel obtainable by these processes.
  • biomass torrefaction condensate as a binding agent or coating agent or other additive for solid biomass-derived material.
  • biomass torrefaction condensate (BTC) is used herein to denote a condensate which can be obtained by conducting a part of the exhaust gas of a biomass torrefaction process, as further described below, containing organic volatiles and water, through a condenser and collecting organic condensate, and optionally water.
  • the BTC can also be used as a binding agent or coating agent or other additive for other materials such as fly ash, char and/or charcoal, although not limited thereto.
  • the BTC is a suitable biobased feedstock for or additive to a wide range of chemicals and materials. This includes for example bio-bitumen, and resins, which can be used as additives, e.g. adhesives, fillers, binders, in products like pavings, floorings (e.g. linoleum), or construction materials such as chipboard, together with oils, cork, wood dust, wood chips, other organic or inorganic fillers etc.
  • the BTC can also be used as phenol substitutes in wood resins (phenol-formaldehyde resins) or as a substitute for high value phenolic compounds like guiacols, syringols and alkylated phenols.
  • the BTC can be present as a final product as well as a fraction in the final products at a level of between 0.5 and 50 wt.%, preferably 1-25 wt.%, most preferably 2-12 wt.%, especially in shaped products such as sheets, plates, tiles, bricks, etc., in addition to 5-95 wt.%, preferably 20-90 wt.% of one or more of oils, cork, wood dust, wood chips, other organic or inorganic fillers etc.
  • the properties of the BTC as an additive can be tuned by adjusting the material and parameters: types of starting biomass (e.g. coniferous wood or deciduous wood, straw or other agricultural residues, mixtures thereof), degree of pre-drying, torrefaction temperatures, torgas cycle ratio, cooling temperatures, etc.
  • types of starting biomass e.g. coniferous wood or deciduous wood, straw or other agricultural residues, mixtures thereof
  • degree of pre-drying e.g. coniferous wood or deciduous wood, straw or other agricultural residues, mixtures thereof
  • degree of pre-drying e.g. coniferous wood or deciduous wood, straw or other agricultural residues, mixtures thereof
  • torrefaction temperatures e.g. coniferous wood or deciduous wood, straw or other agricultural residues, mixtures thereof
  • torgas cycle ratio e.g. by extraction or distillation
  • the BTC is condensed at a temperature which is between 100°C above and 50°C below the condensation temperature of water, preferably between 90°C above and 20°C below the condensation temperature of water, more preferably between 80°C above and 10°C below the condensation temperature of water, most preferably between 60°C above and the condensation temperature of water.
  • the temperatures and pressure are selected in such a manner that, depending on the content of water and organic molecules in the gas, most of the organic material is condensed, while most, but not necessarily all water remains in the vapour phase.
  • the BTC itself preferably comprises all material which is condensable between the torrefaction temperature (200-350°C, especially 240-320°C, see below) and 50°C below the condensation temperature of water, most preferably between the torrefaction temperature and the condensation temperature of water (e.g. 100°C at atmospheric conditions).
  • the heavier components of the BTC i.e. the components which are condensed first, were found to be highly valuable in the use according to the invention.
  • the BTC is a multi-component material comprising lignin degradation products and other biomass-derived organic molecules. Their molecular weights will be broadly in the range of 30-220 Da, in particular 60-170 Da.
  • the BTC contains at least 5 wt.%, up to 70 wt.%, in particular between 10 and 40 wt.% of phenolic compounds, in particular having the formula R 1 R 2 CeH 3 OH, wherein R 1 is methoxy, ethoxy or Ci-C 3 alkyl or alkenyl, and R 2 is hydrogen, hydroxyl or methoxy.
  • the BTC has a condensation temperature range between below the condensation temperature of water up to the torrefaction temperature, e.g. at atmospheric pressure 50-350 °C, preferably 100-320°C. The fraction which has a condensation temperature range (boiling point range) between 150 and 300°C is most valuable.
  • a proportion of the BTC preferably is low-boiling, i.e. having a boiling range between 65 and 150°C.
  • diluents such as alcohols (ethanol, butanol) or aromatics, such as toluene and xylenes, or other moderately polar and inoffensive solvents can be used to provide the BTC with the required viscosity so as allow convenient processing, e.g. at a level of between 3 and 30 wt.% of the (dry) BTC.
  • the BTC may comprise up to 80 wt% water, but preferably less, e.g. below 50 wt.%.
  • the water content may vary depending on the temperature at which the BTC is condensed. Where necessary to lower the water content of the agent, the temperature at which the BTC is condensed may be between 0°C and 100°C above the condensation temperature of water, in particular between 5°C and 80°C above the condensation temperature of water. Alternatively, further cooling and separation of water may be used. On the other hand, where the water content is too low, water may be added before using the condensate as a binding or coating agent. The amount of water can e.g.
  • Water may also be added separately, directly to the densification process, for example directly into the pelletisation apparatus. Water may be added as liquid or as vapour.
  • the BTC binding or coating agent may contain further additives, which enhance the processability or homogeneity of the agent.
  • Such further additives may include organic solvents, such as alcohols (e.g. ethanol, butanol), glycols (ethylene glycol propylene glycol), or higher polyols such as glycerol.
  • alcohols e.g. ethanol, butanol
  • glycols ethylene glycol propylene glycol
  • polyols such as glycerol.
  • the use of such further additives is not always necessary, and if used, their level is preferably below 50 wt.% based on the total weight of the agent, in particular between 0 and 20 wt.% thereof.
  • such additives may preferably be low-grade, i.e. contain water or further organic components, preferably excluding heteroatoms such as sulphur, halogens, metals etc.
  • a weight ratio of below 1 :4 When used as a binding agent, it is preferably used at between 1 :99 and 1 :7 (1-12.5%), more preferably 1 :99 to 1 :9 (1-10%) to the solid material.
  • the ratio When used as a coating agent, the ratio is preferably between 1 :24 and 1 :4, while ratios between 1 : 19 and 1 :7 are preferred.
  • Any solid or solid-like biomass or other (semi) solid carbonaceous material as defined below, having insufficient resistance to dusting or rupture or having insufficient wear- and/or water resistance, may be treated with the BTC as a binding or coating agent.
  • Examples include wood dust, wood chips, as such or in compressed form, agricultural waste etc.
  • the biomass may be treated as such.
  • Particularly useful is a solid biomass-derived material which is thermally pre-treated so as to increase its value as a biomass-derived fuel, most in particular by torrefaction of the biomass. As a result of the thermal pre-treatment, the biomass has lost part or most of the effectiveness of its natural binding agents, such as lignin and/or resin. In this way two components from the same process are efficiently used, i.e.
  • the torrefied solid mass as the basic biomass material and the condensed volatiles (BTC) as the binder or coating agent.
  • BTC condensed volatiles
  • other carbonaceous material with insufficient intrinsic binding agents such as fly ash, char or charcoal, can also be advantageously treated according to the invention.
  • biomass denotes organic material derived from plant in any form, in particular wood, straw and other plant residues and the like.
  • biomass also encompasses peat, manure, recycled wood, as well as algae and seaweeds.
  • a "carbonaceous material” is any material which contains substantial amounts, specifically at least 10 wt.%, in particular at least 25 wt.%), of carbon, wherein fully oxidised carbon (i.e. in carbon dioxide or carbonate form) is excluded.
  • carbonaceous material encompasses biomass and fossil carbon-containing materials such as coal, oil residues and other non or incompletely combusted (solid) combustibles.
  • biomass which consists partly or largely, say at least 50 wt%> (dry weight basis), of wood, herbaceous plants, agricultural (plant) residues or combinations thereof.
  • at least 70 wt% consists of biomass-derived material, in particular of wood and or herbaceous plants, most preferably at least 50 wt% of wood.
  • the wood may be hard wood (deciduous) or soft wood (coniferous) or any mixture thereof. Any remaining part of the biomass may originate from straw or other agricultural or sylvicultural waste, or other organic waste having acceptable levels of hazardous contaminants such as halogen compounds, and the like.
  • Non-biomass, i.e. fossil derived organic material may be admixed, but preferably at minor levels, e.g. below 25 wt.% only.
  • the invention concerns a process for producing a wear- and water-resistant solid biomass-derived fuel, comprising combining a solid biomass- derived material with a BTC as described above.
  • the content of BTC may be between 1 and 25 wt.%, based on the weight of the final product.
  • the BTC When used as a binder, it can be mixed with the solid biomass in the described ratios.
  • the precise ratio can be determined by the skilled person as a function of the further processing steps and the ultimate use of the solid material. Likewise, the precise water level can be adjusted so as to achieve optimum results.
  • Mixing can be done separately, in a distinct mixing equipment, or it can be part of the further densification steps, such as pelleting, briquetting or tabletting.
  • the invention also applies to torrefied or heat-treated biomass that undergoes densification. In particular it is of use in pelletisation and briquetting as described below.
  • the invention may also be applied to tabletting or any other form of densification.
  • Pelletisation can be carried out in conventional pelletising equipment such as used for producing wood pellets from chips or animal feed pellets.
  • the binding agent may be directly fed into the pelletiser or prior to entering the pelletiser.
  • the BTC is produced in situ, i.e. the gas flow, or part of it, containing the organic volatiles of the torrefaction process, is brought in contact with the solid (torrefied) biomass at relatively low temperatures, resulting in condensation of the organic volatiles onto the solid biomass.
  • the organic material volatilised during torrefaction of biomass is directly condensed onto the solid biomass-derived material.
  • the temperature of the torrefied biomass being subjected to the stream of organic volatiles is chosen as described above for the temperature at which the BTC is condensed, and can be varied depending on the desired amount of water condensation onto the torrefied biomass.
  • the biomass which is subjected to the stream of organic volatiles is between 100°C above and 50°C below the condensation temperature of water, especially between 90°C above and 20°C below, preferably between 80°C above and 10°C below the condensation temperature of water, most preferably between 60°C above and the condensation temperature of water.
  • Briquetting is another form of densification to be used according to the invention.
  • material is enclosed in a space and subsequently force is applied from one direction or more directions.
  • Briquettes are larger than pellets, typically more than 20 mm in diameter. The energy needed to make them is much lower than for pelleting.
  • briquetting is done cold or with heat applied from outside, while in pelleting the material is heated up substantially as a result of the friction in the die.
  • At least three forms of briquetting can be distinguished: i) between two rolls with hemispherical spaces, ii) by compressing in a cycle where the previous briquette is immovably clamped at the exit acting as a temporary fixed wall; iii) extrusion of a single strand, similar to pelleting but with a much larger diameter; the strand is cut into briquettes.
  • the force can be generated hydraulically, from a fly wheel with an eccentrically mounted piston or a feeder screw.
  • the way BTC is used in briquetting is analogous to its use in pelletisation (see above).
  • the BTC When the BTC is used as a coating agent, it is applied onto the solid biomass material after densification using conventional coating technique such as spray-coating, dip-coating etc. The precise amounts of coating agent are determined on the basis of routine adjustment depending on the shape and further characteristics of and requirements for the final material.
  • the BTC When the BTC is used as a bio-based chemical such as bitumen, or resin, for use as a binder, filler, adhesive, lubricant, or the like, it can be combined with other materials such as wood dust or chips, cork, cements, other resins etc., in a manner known per se for conventional binders, fillers, adhesives etc.
  • the invention further encompasses a process for upgrading biomass comprising:
  • step (c) densifying the torrefied solid fraction, either after, before or during combining with the condensate in step (c); when the condensate is used as a binder for the torrefied solid fraction, combining (i.e. mixing) takes place before or during densification, and when the condensate is used as a coating agent for the torrefied solid fraction, combining (i.e. coating) takes place after densification.
  • the torrefaction is performed at a temperature of between 200 and 350°C, preferably between 240 and 350°C, more preferably between 240 and 320°C.
  • the weight ratio between said organic condensate and said torrefied solid fraction is preferably between 1 :4 and 1 :99.
  • no more than 10 wt.%, of other additives than an organic torrefaction condensate is used on the basis of the dry weight of the torrefied mass fraction, preferably less than 5 wt.%.
  • Such less desired additives include starch and other materials that would have to be abstracted from potential food supplies, and fossil-derived polymers and derivatives. If used, they are used at a level of no more than 50 wt.% of the BTC.
  • An acceptable further additive which may be used up to e.g. 20% of the dry weight of the torrefied mass, or up to 50wt.% of the BTC, may be lignin obtained from wood in another way than as a torrefaction condensate.
  • the invention also pertains to a torrefied biomass-derived material, suitable as a fuel, obtainable by the process as described herein.
  • a biomass-derived fuel can be defined by one or more of the following characteristics:
  • iii a specific density between 0.8 and 1.5 kg/dm 3 , preferably between 1.1 and 1.4 kg/dm 3 ;
  • HHV higher heat value
  • LHV lower heat value
  • v. a moisture content of less than 5 wt.%, also after storage at ambient conditions for at least 1 month;
  • a carbon content derived from biomass of at least 75% which can for example be determined by its 14 C content of at least 5.10 "13 (0.5 ppt) on carbon basis; vii. a grindability which is comparable to the grindability of coal, corresponding to a power consumption below 0.5 MJ/ton on a 0.25 mm mesh; viii. stability to ambient (outdoor) conditions for at least 1 month.
  • analyses are typically performed by exposing a 1 kg- sized sample to a set humidity level (working range 0-95 %, typically in the range of 70-95 % relative humidity) at a desired temperature (range -40 to +80 °C, typically 5- 25 °C) over a desired period of time (typically 7 days, though which can be extended to 1 month) in a climate chamber sufficiently large to accommodate several specimens. Samples are drawn after specific time intervals during the period of exposure. The moisture uptake investigations are aided by standard moisture analyses. A visual observation of mold formation or other signs of biologic degradation (discoloration, effluent or gas formation) is also done to check stability.
  • Another rapid test for sufficient stability consists in submerging particles (e.g. pellets) in water of ambient temperature for at least 24 h, in particular 1 week; if the particles can be taken from the water without noticeable softening or other visible change, the stability is rated to be sufficient.
  • a solid fuel produced according to this invention may be made from torrefied biomass and BTC, with less than 5 wt% of other additives present, preferably less than 2 wt%, in particular less than 0.5 wt%.
  • the biomass and the binder, and optionally even a part of the water or the entire water fraction, which are used in the densification process all originate from the biomass which was fed to the torrefaction reaction, and thus less waste is produced.
  • solid fuels produced according to the invention and a densification process according to the invention are more energy and waste efficient than prior art pellets and processes.
  • BTC has improved properties as a binder compared to pyro lysis oil.
  • pyrolysis oil is more acidic than BTC, contains more water and it also does not harden when cooled or tempered.
  • Pyrolysis is performed at higher temperatures than torrefaction, and the condensate of the pyrolysis gas (pyrolysis oil) comprises smaller molecules, i.e. the lignin and hemicelluloses components of the biomass are degraded into smaller molecules, because of the high pyrolysis temperature.
  • This degradation into smaller molecules comprises hydrolysis or decomposition of lignin and hemi- cellulose derivatives, thereby producing phenolic and carboxylic acid moieties and molecules.
  • Torrefaction at elevated temperatures causes more lignin to break down into smaller molecules, which evaporate into the gas phase.
  • the resulting torrefied biomass has a higher calorific value and a higher carbon content than biomass torrefied at lower temperatures, due to this heat treatment.
  • This biomass resembles charcoal more than low-temperature torrefied biomass.
  • densifying torrefied biomass obtained by torrefaction at elevated temperature used to be more problematic, as a result of the lower effectiveness of the lignin residues remaining in the torrefied biomass acting as a binder.
  • BTC as a binder solves this problem, as BTC originates from the same biomass as the torrefied biomass, which is now low in lignin residues. Hence, no other additives are needed for processing, including pelletising or briquetting of the torrefied biomass, resulting in a solid fuel with a very low, if any, content of material which does not originate from the biomass that was fed to the torrefaction chamber.
  • the pellet or briquette according to the invention preferably comprises at most 5 wt% other additives, preferably at most 2 wt% in particular at most 0.5 wt%.
  • other additives that are not present in the solid fuel or in very small amounts comprise materials that are potentially suitable as food components such as starch, fossil derived components, but also although with less drawbacks, minerals such as cement, clay, etc..
  • the solid fuel contains at least 99.5 wt% material that originates from biomass, in particular from a biomass torrefaction process.
  • the torrefaction process can be carried out as described below.
  • the organic material may for instance have a moisture content of 5-15%.
  • the organic material with the residual moisture is introduced into the torrefaction reactor.
  • the material is heated in the substantial absence of oxygen, usually though not necessarily under atmospheric pressure, to a temperature of 200-350 °C, preferably 240-320 °C, more preferably 250- 310 °C, for example 260-300 °C.
  • Torrefaction may begin as soon as the temperature of the material exceeds about 200 °C.
  • the lack of oxygen prevents the material from burning. Instead the material is torrefied, which leads to loss of mass because of the elimination of gases.
  • the torrefying chamber is flushed with a gas substantially free of oxygen, such as a C0 2 , N 2 steam and/or recirculated process gasses.
  • a gas substantially free of oxygen such as a C0 2 , N 2 steam and/or recirculated process gasses.
  • the water content of the organic material provides the majority of the process gas, so that supply of additional process can be avoided.
  • the torrefying chamber, but also the gas transport structure may be kept at a pressure in the range of -0.5 to +20 bar, and in general at a pressure near atmospheric pressure.
  • the gas issuing from the torrefaction reactor is conducted through a cooling chamber downstream from the torrefying chamber gas outlet, to allow condensables to be condensed from the gas, for example in the cooling chamber, to produce the biomass torrefaction condensate (BTC).
  • BTC biomass torrefaction condensate
  • the remaining gas thus obtained from the cooling chamber may then be heated again in a heating chamber to reach a temperature suitable for introduction into the torrefying chamber.
  • Cooling may comprise cooling to a cooling temperature in the range of higher than about 50°C below the dew point of water and lower than the torrefying temperature in the torrefying chamber.
  • the cooling temperature will be around or above the condensation temperature of water, and preferably below about 200 °C.
  • the cooling temperature may be selected from the range of 90-180 °C, such as about 1 10-140 °C; this may especially apply at atmospheric conditions. At pressurised conditions, the selected temperature may be correspondingly higher.
  • the cooling may comprise cooling to a cooling temperature in the range of about 20°C below the boiling point of water and lower than the torrefying temperature in the torrefying chamber.
  • the cooling temperature will be around or above the boiling point of water, and preferably below about 200 °C.
  • the cooling chamber may comprise a receiver, arranged to receive liquid from the cooling chamber and optionally arranged to receive liquid from the heating chamber.
  • the receiver may act as a gas liquid separating device separating liquid droplets and/or aerosols from the gas stream.
  • the receiver may further be connected with a storage vessel.
  • the condensate (BTC) mainly originating from the lignin fraction in the biomass, is used as a binder in the production of biomass-derived fuels.
  • the BTC has a calorific value significantly higher than the original feedstock, typically between 28 and 35 MJ/kg on a dry basis, and an elemental composition similar to the elemental composition of lignins.
  • condensate has a high solubility in ethanol or glycerol and less high solubility in water or hydrocarbon liquids such as diesel. Evaporation of the condensate is only possible without substantial carbonaceous remainder, if it is in the form of aerosols below about 1 micron in diameter.
  • the condensate is not stable at elevated temperatures. For atmospheric conditions, at 100 °C mass loss of around 15 % may occur over a week. At temperatures exceeding 200 °C the condensate may rapidly degrade leaving a carbonaceous residue behind, unless the condensate liquid is in the form of aerosols.
  • a torrefying device to be used according to the invention may comprise: a. a torrefying chamber configured to torrefy organic material, the torrefying chamber further comprising a torrefying chamber gas inlet for a gas and a torrefying chamber gas outlet for removal of torrefying chamber gas from the torrefying chamber;
  • a gas transport structure downstream of the torrefying chamber gas outlet, comprising a cooling chamber, comprising a cooling chamber opening for the separation of BTC, and downstream from the cooling chamber optionally a heating chamber;
  • a gas transport device configured to remove torrefying chamber gas via the torrefying chamber gas outlet from the torrefying chamber and configured to transport torrefying chamber gas through the gas transport structure (at least through the cooling chamber and optionally also through the heating chamber).
  • the liquid material obtained after cooling is used according to the invention as described above and illustrated below. Also the remaining gas may be used. As indicated above, it may partly be reused, and introduced (after heating) to the torrefying chamber, and produced torgas may partly be taken from the loop and combusted in a combustor to provide energy for the system.
  • the torrefying device may further comprise an additional gas source, configured to provide torrefying gas into the torrefying chamber.
  • the amount of BTC produced depends on the feedstock, the cooling temperature in the torgas loop, but more importantly also on the operating temperature of the torrefaction process.
  • the torrefaction temperature is increased, more volatile organic components will be released, providing a different ratio of BTC versus torrefied biomass.
  • the amount of BTC related to the torrefied biomass will be low, in a typical experiment as presented in the table below 0.3%.
  • this amount increases to 2.3 and 4.0%, respectively. Indicative trials at higher temperatures show that percentages above 10% can also be obtained. The results are presented in Table 1.
  • Table 1 Mass balance of test with wood chips
  • BTC 2.83 kg BTC was mixed with 1.12 kg ethanol at ambient temperature to produce a 72 % solution.
  • the liquid was a thick dark fluid.
  • 50 ml of this mixture was added to 2.5 kg of solid material torrefied at 265°C. Effectively, the batch contained 1.4 wt% BTC on the torrefied material.
  • the batch was left for several hours.
  • a reference batch was prepared by adding 20 gram water to 400 gram solid material. The total moisture content was about 11 wt%, which was found to be suitable for making pellets in previous tests.
  • the tests were performed in a pelletising machine with a die of 4.8 mm.
  • the reference material was used for flushing the machine.
  • the input was switched to material with added BTC.
  • the output data are presented in Table 2.
  • Ethanol was added only to facilitate mixing of the BTC and was evaporated during pelleting. When operating at elevated temperatures, the BTC is sufficiently fluid to be blended without ethanol.
  • the torrefied wood and the condensates were used to produce pellets using a single pellet Pronto press.
  • the amounts of condensate applied were varied according to a ratio of condensate to torrefied wood of 2.5, 5.0 and 7.5 wt.%.
  • a ratio of condensate to torrefied wood 2.5, 5.0 and 7.5 wt.%.
  • Table 4 summarises the pellet density in kg/m 3 after pelletisation at 160°C. Higher density indicates lower porosity and higher strength. When marked with an x, good pelletisation was not possible. Pelletisation was performed at lower temperatures as well (60, 80, 100, 120 and 140°C) showing all the same result, whereas higher torrefaction temperatures lead to lower densities, adding BTC as binder can increase the density again. However, there seems to be a limit to the amount of BTC that can be applied, which is temperature dependent and corresponds closely to the amount of BTC actually produced during torrefaction. When adding more BTC, the BTC is pressed out of the pellet and the pellet becomes sweaty.
  • BTC BTC
  • An organic binder such as BTC is often needed for producing a solid biomass-derived fuel (e.g. as a coal substitute) of desired quality (Example 2).
  • a solid biomass-derived fuel e.g. as a coal substitute
  • product qualities cause the torrefied solid to be less suitable as a solid fuel in terms of processability (grindability etc.), stability and caloric value, even with use of a binder.
  • the amount of BTC produced at lower temperatures is not sufficient to achieve optimum performance after binding when using the same BTC as a binder (Example 1).
  • Amounts of BTC produced, but also amounts of non-condensed gas, are proportional to the torrefaction temperature, at least over the range of 235-300°C (Example 1), while density of the solid material decreases (Example 3).
  • the composition of the BTC changes with increasing temperature, while at temperatures above about 300°C, and more seriously at temperatures above 350°C binding capabilities will decrease because of excessive degradation of lignin.
  • Amounts of BTC that can be incorporated as a binder into solid material resulting from torrefaction increases with temperature, and the binder increases the density and strength of the solid material (Example 1).

Abstract

Le produit obtenu par condensation d'un matériau organique volatilisé pendant la torréfaction d'une biomasse peut être utilisé en tant qu'agent de liaison ou agent de revêtement ou bien en tant qu'additif pour matériau carboné solide pour produire un combustible solide résistant à l'usure et à l'eau, lequel peut être dérivé pour une large part ou dans sa totalité de la biomasse. Le produit ainsi obtenu convient comme combustible solide (partiellement) renouvelable.
PCT/NL2012/050541 2011-08-01 2012-07-31 Utilisation d'un condensat de torréfaction WO2013019111A1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
NL2007206A NL2007206C2 (en) 2011-08-01 2011-08-01 Use of torrefaction condensate.
NL2007206 2011-08-01
NL2008308 2012-02-17
NL2008308 2012-02-17

Publications (1)

Publication Number Publication Date
WO2013019111A1 true WO2013019111A1 (fr) 2013-02-07

Family

ID=46727538

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NL2012/050541 WO2013019111A1 (fr) 2011-08-01 2012-07-31 Utilisation d'un condensat de torréfaction

Country Status (2)

Country Link
AR (1) AR087425A1 (fr)
WO (1) WO2013019111A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180037835A1 (en) * 2012-07-19 2018-02-08 Michael A. Lake Energy pellet
WO2019002690A1 (fr) 2017-06-28 2019-01-03 Oy Lunawood Ltd Procédé et appareil pour l'extraction de produits à partir d'un processus de traitement
US10995274B2 (en) 2015-07-21 2021-05-04 British Columbia Biocarbon Ltd. Biocoal fuel product and processes and systems for the production thereof
WO2021117798A1 (fr) * 2019-12-10 2021-06-17 日本製紙株式会社 Matériau de résine pour moulage et son procédé de fabrication

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102005049375A1 (de) * 2005-10-15 2007-04-26 Forschungszentrum Karlsruhe Gmbh Verfahren zur Herstellung und Vorbereitung von Schnellpyrolyseprodukten aus Biomasse für eine Flugstrom Druckvergasung
WO2007078199A1 (fr) 2006-01-06 2007-07-12 Stichting Energieonderzoek Centrum Nederland Processus et dispositif de traitement de biomasse
US20090151251A1 (en) * 2007-12-17 2009-06-18 Range Fuels, Inc. Methods and apparatus for producing syngas and alcohols
CA2681282A1 (fr) 2008-10-03 2010-04-03 Wyssmont Company Inc. Systeme et methode de sechage et de thermotransformation
US20100083530A1 (en) 2008-10-03 2010-04-08 Wyssmont Co. Inc. System and method for drying and torrefaction
EP2236587A1 (fr) * 2009-04-02 2010-10-06 General Electric Company Boues biologiques modifiées et procédé pour sa production et sa gazéification
US20100251616A1 (en) * 2009-04-01 2010-10-07 Paoluccio John A Sequencing retort liquid phase torrefication processing apparatus and method
WO2010129988A1 (fr) * 2009-05-15 2010-11-18 Anthroterra Pty Ltd Complexe de biochar

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102005049375A1 (de) * 2005-10-15 2007-04-26 Forschungszentrum Karlsruhe Gmbh Verfahren zur Herstellung und Vorbereitung von Schnellpyrolyseprodukten aus Biomasse für eine Flugstrom Druckvergasung
WO2007078199A1 (fr) 2006-01-06 2007-07-12 Stichting Energieonderzoek Centrum Nederland Processus et dispositif de traitement de biomasse
US20090151251A1 (en) * 2007-12-17 2009-06-18 Range Fuels, Inc. Methods and apparatus for producing syngas and alcohols
CA2681282A1 (fr) 2008-10-03 2010-04-03 Wyssmont Company Inc. Systeme et methode de sechage et de thermotransformation
US20100083530A1 (en) 2008-10-03 2010-04-08 Wyssmont Co. Inc. System and method for drying and torrefaction
US20100251616A1 (en) * 2009-04-01 2010-10-07 Paoluccio John A Sequencing retort liquid phase torrefication processing apparatus and method
EP2236587A1 (fr) * 2009-04-02 2010-10-06 General Electric Company Boues biologiques modifiées et procédé pour sa production et sa gazéification
WO2010129988A1 (fr) * 2009-05-15 2010-11-18 Anthroterra Pty Ltd Complexe de biochar

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180037835A1 (en) * 2012-07-19 2018-02-08 Michael A. Lake Energy pellet
US10995274B2 (en) 2015-07-21 2021-05-04 British Columbia Biocarbon Ltd. Biocoal fuel product and processes and systems for the production thereof
WO2019002690A1 (fr) 2017-06-28 2019-01-03 Oy Lunawood Ltd Procédé et appareil pour l'extraction de produits à partir d'un processus de traitement
EP3645143A4 (fr) * 2017-06-28 2021-05-05 Oy Lunawood Ltd Procédé et appareil pour l'extraction de produits à partir d'un processus de traitement
US11766626B2 (en) 2017-06-28 2023-09-26 Oy Lunawood Ltd Method and apparatus to extract products from heat treatment process
WO2021117798A1 (fr) * 2019-12-10 2021-06-17 日本製紙株式会社 Matériau de résine pour moulage et son procédé de fabrication
CN114901757A (zh) * 2019-12-10 2022-08-12 日本制纸株式会社 成型用树脂材料及其制造方法

Also Published As

Publication number Publication date
AR087425A1 (es) 2014-03-19

Similar Documents

Publication Publication Date Title
Awalludin et al. An overview of the oil palm industry in Malaysia and its waste utilization through thermochemical conversion, specifically via liquefaction
Tahir et al. Demonstrating the suitability of canola residue biomass to biofuel conversion via pyrolysis through reaction kinetics, thermodynamics and evolved gas analyses
Kim et al. Upgrading the characteristics of biochar from cellulose, lignin, and xylan for solid biofuel production from biomass by hydrothermal carbonization
Kim et al. Investigation of physicochemical properties of biooils produced from yellow poplar wood (Liriodendron tulipifera) at various temperatures and residence times
Benavente et al. Torrefaction of olive mill waste
Zhang et al. Upgrading of biomass pellets by torrefaction and its influence on the hydrophobicity, mechanical property, and fuel quality
Yusuf et al. Characterization of Ugandan biomass wastes as the potential candidates towards bioenergy production
US20210284913A1 (en) Biocoal fuel product and processes and systems for the production thereof
Zhang et al. Effect of pretreatment on chemical characteristic and thermal degradation behavior of corn stalk digestate: comparison of dry and wet torrefaction
Oyebode et al. Impact of torrefaction process temperature on the energy content and chemical composition of stool tree (Alstonia congenisis Engl) woody biomass
Dhakate et al. Rice straw biomass to high energy yield biocoal by torrefaction
Yang et al. Pyrolysis process and characteristics of products from sawdust briquettes
Medic Investigation of torrefaction process parameters and characterization of torrefied biomass
Kang et al. Codensification of agroforestry residue with bio-oil for improved fuel pellets
WO2013019111A1 (fr) Utilisation d'un condensat de torréfaction
Ronsse Biochar production
US20140075833A1 (en) Compositions and methods for composite fuels
Setter et al. Evaluation of the physical-mechanical and energy properties of coffee husk briquettes with kraft lignin during slow pyrolysis
Ma et al. Integration of torrefaction and in-situ pelletization for biodried products derived from municipal organic wastes: The influences of temperature on fuel properties and combustion behaviours
Javanmard et al. A comprehensive overview of the continuous torrefaction method: Operational characteristics, applications, and challenges
Hooi et al. Laboratory-scale pyrolysis of oil palm pressed fruit fibres
WO2019118565A1 (fr) Briquettes de biomasse torréfiées et procédés associés
Amponsem et al. Cleaner energy potential analysis for composite biomass residues from decentralized sawmills in Ghana-A case study for Oforikrom Municipality
JP2011093980A (ja) 成型炭の製造方法
Fernandez-Lopez et al. Catalytic and non-catalytic pyrolysis of biologically treated manure.

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12750860

Country of ref document: EP

Kind code of ref document: A1

DPE1 Request for preliminary examination filed after expiration of 19th month from priority date (pct application filed from 20040101)
NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 12750860

Country of ref document: EP

Kind code of ref document: A1